Aromatic polycarbonate oligomer solid

ABSTRACT

The purpose of the present invention is to provide an aromatic polycarbonate oligomer solid with substantially reduced low-molecular-weight components, no or a substantially reduced amount of chlorine-containing compounds, high loose bulk density, and ease of handling. The aromatic polycarbonate oligomer solid contains a repeating unit represented by formula (1), has a weight average molecular weight of 500 to 10,000, low-molecular-weight components less than or equal to 5.0 area % measured with high-speed liquid chromatography, and a loose bulk density of greater than or equal to 0.30 g/cm 3 :

TECHNICAL FIELD

The present invention relates to an aromatic polycarbonate oligomersolid, and particularly relates to an aromatic polycarbonate oligomersolid containing 1,1-bis(4-hydroxyphenyl)-1-phenylethane and a carbonateprecursor as raw materials.

BACKGROUND ART

The polycarbonate oligomer is widely used, for example, as anintermediate raw material in the production of a high molecular weightpolycarbonate by an interfacial polymerization method, as a raw materialin the production of a high molecular weight polycarbonate by a meltpolymerization method or a solid phase polymerization method, or as apolymer modifier such as a surface modifier, a flame retardant, anultraviolet absorber, a flowability modifier, a plasticizer, or acompatibilizer for resin alloy. In recent years, the requiredperformance of polycarbonate oligomers has become increasingly diverseand severe, and further improvements have been demanded forpolycarbonate oligomers other than bisphenol A type polycarbonateoligomers. Among them, aromatic polycarbonate oligomers containing1,1-bis(4-hydroxyphenyl)-1-phenylethane and a carbonate precursor as rawmaterials require further improvement in performance.

On the other hand, in a method of producing a polycarbonate oligomer, aninterfacial polymerization method in which an aromatic dihydroxycompound and phosgene are used as raw materials and reacted in amethylene chloride solvent to produce a polycarbonate oligomer as anintermediate raw material of a high molecular weight polycarbonate ismainly used, and usually there is employed a method of blowing phosgeneinto an alkaline aqueous solution of bisphenols to produce apolycarbonate oligomer having a reactive chloroformate group, mixing thepolycarbonate oligomer and the alkaline aqueous solution of bisphenols,and advancing a polycondensation reaction in the presence of apolymerization catalyst such as a tertiary amine. However, theinterfacial polymerization method has problems such as that toxicphosgene must be used, that equipment is corroded by chlorine-containingcompounds such as the by-produced hydrogen chloride and sodium chloride,and methylene chloride used in large amount as a solvent, and that it isdifficult to separate impurities such as sodium chloride which adverselyaffect polymer physical properties and residual methylene chloride.Thus, a method of producing a polycarbonate oligomer by a melttransesterification method using an aromatic dihydroxy compound and acarbonic acid diester as raw materials has also been put into practicaluse. However, although the melt transesterification method has solvedthe above problems in the interfacial polymerization method, there is aproblem that the produced oligomer contains a large amount of residualmonomers and low molecular weight components.

On the other hand, among polycarbonate oligomers obtained by theinterfacial polymerization method, as a polycarbonate oligomercontaining, as a monomer component, a bisphenol compound other thanbisphenol A (hereinafter sometimes referred to as special bisphenol),polycarbonate oligomers respectively containing, as a monomer component,2,2-bis(4-hydroxy-3-methylphenyl)propane (Patent Literature 1),1,1-bis(4-hydroxyphenyl)cyclohexanes (Patent Literature 2), and9,9-bis(4-hydroxyphenyl)fluorene (Patent Literature 3) are known.

However, since these special bisphenol polycarbonate oligomers areproduced by the interfacial polymerization method, when they are used asprepolymers or additives, as described above, corrosion of equipment dueto residual chlorine-containing compounds and deterioration of polymerphysical properties are concerned.

As aromatic polycarbonate oligomers obtained by the melttransesterification method, polycarbonate oligomer of bisphenol A andpolycarbonate oligomers of special bisphenol such as1,1-bis(4-hydroxyphenyl)cyclohexane are known (Patent Literatures 4 and5).

However, these polycarbonate oligomers are either taken out as they areafter the reaction or only subjected to heat treatment, and since theyhave not undergone a purification process, low molecular weightcomponents formed during the reaction remain. Accordingly, when thepolycarbonate oligomers are directly used for polycarbonate rawmaterials for melt polymerization or solid phase polymerization, thereis a high possibility that troubles such as line clogging occur due tovolatilization of low molecular weight components in equipment. Further,there is a concern that impact strength may be lowered and adhesion to amold may occur when a high molecular weight polycarbonate is used.Furthermore, if a large amount of low molecular weight components remainin the polycarbonate oligomer, storage stability is poor, anddeterioration of qualities such as coloration is concerned.

In the prior art, a method of isolating an aromatic polycarbonateoligomer starting from 1,1-bis(4-hydroxyphenyl)-1-phenylethane and acarbonate precursor as a solid from a final reaction product is notknown; however, as a method of isolating an aromatic polycarbonateoligomer starting from 2,2-bis(4-hydroxyphenyl) propane and a carbonateprecursor as a solid from a final reaction product, there is known amethod in which a dichloromethane solution of a polycarbonate oligomerof 2,2-bis(4-hydroxyphenyl) propane obtained by an interfacialpolymerization method is added dropwise to methanol to precipitate(Patent Literature 1).

However, the polycarbonate oligomer obtained by the above method isproduced by the interfacial polymerization method, and in addition,precipitation is carried out using a dichloromethane solution;therefore, a chlorine-containing compound such as dichloromethaneremaining in the polycarbonate oligomer cannot be completely removed,and as described above, corrosion of equipment and deterioration ofpolymer physical properties are concerned. In addition, thepolycarbonate oligomer of 2,2-bis(4-hydroxyphenyl) propane obtained froma solvent system using the above tetrahydrofuran and dichloromethanesolution has low bulk density and thus is difficult to handle, and whenthe polycarbonate oligomer is used as a reaction raw material, there isalso a problem that not only more energy is required for charging thepolycarbonate oligomer into a reaction vessel, but also the reactionvessel itself must be made larger.

As a method of isolating a polymer as a solid from a high molecularweight polycarbonate final reaction product, there is known a method inwhich 1,1-bis(4-hydroxyphenyl)-1-phenylethane and a carbonate precursorare used as raw materials, a dichloromethane solution of high molecularweight polycarbonate obtained by polymerization according to aninterfacial polymerization method is dropped into hot water, and asolvent is removed by evaporation to isolate the polymer as a solid(Patent Literature 6).

However, similar to the case of the oligomer described above, inaddition to the production using the interfacial polymerization method,precipitation is carried out using a dichloromethane solution;therefore, a chlorine-containing compound such as dichloromethaneremaining in the polycarbonate cannot be completely removed, and asdescribed above, corrosion of equipment and deterioration of polymerphysical properties due to the remaining chlorine-containing compoundare concerned.

Furthermore, only a solvent in a polymerization reaction solution isremoved, and all components other than the solvent are solidified asthey are. Since there is no purification effect, low molecular weightcomponents generated during the reaction remain, so that, as describedabove, storage stability is poor, and quality deterioration such ascoloring is concerned.

CITATION LIST Patent Literature

-   -   Patent Literature 1: Japanese Unexamined Patent Application        Publication No. 2001-163967    -   Patent Literature 2: Japanese Unexamined Patent Application        Publication No. 2007-119691    -   Patent Literature 3: Japanese Unexamined Patent Application        Publication No. 2002-220455    -   Patent Literature 4: Japanese Unexamined Patent Application        Publication No. 2003-192779    -   Patent Literature 5: Japanese Unexamined Patent Application        Publication No. 2009-180760    -   Patent Literature 6: Japanese Unexamined Patent Application        Publication No. 2011-046769

SUMMARY OF THE INVENTION Technical Problems

The present invention has been made against the background of the abovecircumstances in the polycarbonate oligomer, and it is an object of thepresent invention to provide a solid of an aromatic polycarbonateoligomer containing 1,1-bis(4-hydroxyphenyl)-1-phenylethane and acarbonate precursor as raw materials. The solid has a suitable molecularweight for improving reactivity without increasing viscosity. Inaddition, in the solid, low molecular weight components are remarkablyreduced, and the chlorine-containing compound is not present or isremarkably reduced. Further, loose bulk density in the solid is high,and the solid is, for example, an easy-to-handle powder solid.

Solution to Problems

As a result of intensive studies to solve the above-mentioned problems,the present inventors have found that, in an aromatic polycarbonateoligomer containing 1,1-bis(4-hydroxyphenyl)-1-phenylethane and acarbonate precursor as raw materials, oligomers of a final reactionproduct are precipitated or subjected to slurry treatment using aspecific solubilizing solvent or a specific precipitating solvent andare dried, so that it is possible to obtain a solid in which lowmolecular weight components are remarkably reduced, thechlorine-containing compound is not present or is remarkably reduced,and loose bulk density is high and which is an easy-to-handle powder orthe like. This has led to the completion of the present invention.

The present invention is as described below.

1. An aromatic polycarbonate oligomer solid including a repeating unitrepresented by the following formula (1) and having a weight averagemolecular weight of 500 to 10000, a low molecular weight component of5.0 area % or less as measured by high performance liquidchromatography, and a loose bulk density of 0.30 g/cm³ or more,

2. An aromatic polycarbonate oligomer solid obtained from an aromaticdihydroxy compound represented by the following formula (2) and acarbonic acid diester and having a weight average molecular weight of500 to 10000, a low molecular weight component of 5.0 area % or less asmeasured by high performance liquid chromatography, and a loose bulkdensity of 0.30 g/cm³ or more,

Advantageous Effects of Invention

When the weight average molecular weight of the aromatic polycarbonateoligomer solid of the present invention is 500 to 10000, the viscosityis not increased, and the reactivity is improved. Further, thechlorine-containing compound is not present or is remarkably reduced,corrosion of equipment can be suppressed, and in addition, the lowmolecular weight component is 5.0 area % or less as measured by highperformance liquid chromatography; therefore, deterioration of qualitiessuch as coloration due to oxidation or the like is prevented, andstorage stability is excellent.

Further, when polycarbonate is produced by the melt polymerizationmethod or solid phase polymerization method using the polycarbonateoligomer solid of the present invention, since the amount of lowmolecular weight components is extremely small, volatile components inequipment are reduced, and it is expected that troubles such as lineclogging can be prevented and that a purification process of removingthe low molecular weight components from the resultant polycarbonateresin can be unnecessary or simplified.

Furthermore, since the solid has a loose bulk density of 0.30 g/cm³ ormore, it is easy to handle, and in the use as a reaction raw material,the capacity of a reaction vessel can be smaller, and productivity isimproved.

DESCRIPTION OF EMBODIMENTS

Hereinafter, an aromatic polycarbonate oligomer solid of the presentinvention will be described in detail.

The aromatic polycarbonate oligomer solid of the present inventioncontains a repeating unit represented by the following formula (1) andhas a weight average molecular weight of 500 to 10000, a low molecularweight component of 5.0 area % or less as measured by high performanceliquid chromatography, and a loose bulk density of 0.30 g/cm³ or more,

A method of producing an aromatic polycarbonate oligomer according tothe present invention is not particularly limited, and anyconventionally known method can be used. Specific examples thereofinclude an interfacial polymerization method, a melt transesterificationmethod, a solid phase polymerization method, a cyclic carbonate compoundring-opening polymerization method, and a pyridine method. Among them,the interfacial polymerization method and the melt transesterificationmethod using aromatic dihydroxy compounds and a carbonate precursor asraw materials are preferred.

In the production of an aromatic polycarbonate oligomer according to thepresent invention, a raw material corresponds to1,1-bis(4-hydroxyphenyl)-1-phenylethane represented by the followingformula (2),

In the aromatic dihydroxy compound to be used as the raw material of thearomatic polycarbonate oligomer according to the present invention, aslong as the effect of the present invention is not impaired, a dihydroxycompound such as bisphenol A, other than1,1-bis(4-hydroxyphenyl)-1-phenylethane represented by the above formula(2), may be used as a copolymerization material.

In the case of using a copolymerization raw material, in all thedihydroxy compounds, a proportion of a dihydroxy compoundcopolymerization raw material, other than the mainly used1,1-bis(4-hydroxyphenyl)-1-phenylethane represented by the above formula(2), is in the range of 0 to 30 mol %, preferably in the range of 0 to20 mol %, more preferably in the range of 0 to 10 mol %, still morepreferably in the range of 0 to 5 mol %, particularly preferably in therange of 0 to 2 mol %.

As a carbonate precursor to be reacted with the aromatic dihydroxycompound, carbonyl halide, carbonate ester, haloformate, and the likeare used. Specific examples include phosgene; carbonic acid diesterssuch as diaryl carbonates such as diphenyl carbonate and ditolylcarbonate and dialkyl carbonates such as dimethyl carbonate and diethylcarbonate; and dihaloformates of dihydric phenols. These carbonateprecursors may be used alone or in combination of two or more.

Further, these carbonate precursors are usually selected appropriatelyaccording to the production process. In obtaining the aromaticpolycarbonate oligomer according to the present invention, phosgene ispreferable in the interfacial polymerization method, carbonic aciddiester is preferable in the melt transesterification method, anddiphenyl carbonate is particularly preferable.

The aromatic polycarbonate oligomer according to the present inventionhas a weight average molecular weight of 500 to 10000, preferably 1000to 9000, more preferably 1500 to 8500, still more preferably 2000 to8000. When the aromatic polycarbonate oligomer has such a molecularweight, the viscosity is not increased, and the reactivity is alsoimproved.

The low molecular weight component according to the present invention isa transesterification condensate mainly having a degree ofpolymerization of 2 or less, measured by high performance liquidchromatography analysis (by high performance liquid chromatographyanalysis area %), and, in addition, is a component containing lowmolecular compounds such as a raw material monomer residue, a phenoldistillation residue which is a reaction product, and a solvent duringreaction/purification. Specifically, the transesterification condensateis a compound having an absolute molecular weight of not more than anabsolute molecular weight of a compound obtained by condensation of twomolecules of an aromatic dihydroxy compound and three molecules of acarbonate precursor, and although the molecular weight varies dependingon the aromatic dihydroxy compound and the carbonate precursor which arethe raw materials of the above formula (1), when an aromatic dihydroxycompound is 1,1-bis(4-hydroxyphenyl)-1-phenylethane represented by theabove formula (2), and the carbonate precursor is diphenyl carbonate andis a single homopolymerization, the transesterification condensate is acompound having an absolute molecular weight of 846 or less of a dimerin which both ends are phenyl groups.

If such a low molecular weight component is exemplified and assumed by achemical formula, when the aromatic dihydroxy compound is1,1-bis(4-hydroxyphenyl)-1-phenylethane and the carbonate precursor isdiphenyl carbonate, examples thereof include the following compound.

Measurement conditions of the low molecular weight component accordingto the present invention by high performance liquid chromatographyanalysis are conditions under which the low molecular weight componentis separated from a compound having an absolute molecular weight of morethan that. When the polycarbonate oligomer of the present invention isspecified, the area % of the low molecular weight component is measuredusing a 254 nm absorbance photometric detector.

The content of the low molecular weight component contained in thearomatic polycarbonate oligomer according to the present invention is5.0 area % or less, preferably 4.0 area % or less, more preferably 3.0area % or less, still more preferably 2.0 area % or less, particularlypreferably 1.0 area % or less as measured by high performance liquidchromatography under the above conditions.

In consideration of the yield, the content of the low molecular weightcomponent contained in the aromatic polycarbonate oligomer according tothe present invention is preferably 0.01 area % or more, more preferably0.05 area % or more, still more preferably 0.1 area % or more asmeasured by high performance liquid chromatography under the aboveconditions.

The loose bulk density of the aromatic polycarbonate oligomer solid ofthe present invention is 0.30 g/cm³ or more, preferably 0.31 g/cm³ ormore, more preferably 0.32 g/cm³ or more, and preferably 0.90 g/cm³ orless, more preferably 0.80 g/cm³ or less, still more preferably 0.70g/cm³ or less, particularly preferably 0.65 g/cm³ or less.

Among the methods for producing an aromatic polycarbonate oligomeraccording to the present invention, first, a method of obtaining thearomatic polycarbonate oligomer by the melt transesterification methodwill be described. In the melt transesterification method, aconventionally known method using an aromatic dihydroxy compound and acarbonic acid diester as raw materials can be used.

For example, the reaction for obtaining an aromatic polycarbonateoligomer when the starting aromatic dihydroxy compound is1,1-bis(4-hydroxyphenyl)-1-phenylethane and the starting carbonic aciddiester is diphenyl carbonate is shown by the reaction formula.

The melt transesterification reaction is carried out by stirring anaromatic dihydroxy compound and a carbonic acid diester in the presenceof a catalyst while heating under an inert gas atmosphere at normalpressure or reduced pressure and distilling out phenol to be formed.

Specific examples of the carbonic acid diester to be reacted with thearomatic dihydroxy compound include diaryl carbonate such as diphenylcarbonate, ditolyl carbonate, or bis(m-cresyl)carbonate, dialkylcarbonate such as dimethyl carbonate, diethyl carbonate, or dicyclohexylcarbonate, alkylaryl carbonate such as methyl phenyl carbonate, ethylphenyl carbonate, or cyclohexyl phenyl carbonate, and dialkenylcarbonate such as divinyl carbonate, diisopropenyl carbonate, ordipropenyl carbonate. Preferred is diaryl carbonate, and particularlypreferred is diphenyl carbonate.

It is possible to usually obtain an aromatic polycarbonate oligomer inwhich a desired molecular weight and the amount of terminal hydroxylgroups are adjusted by adjusting a mixing ratio of the carbonic aciddiester and the aromatic dihydroxy compound and the degree of pressurereduction during transesterification reaction.

In the mixing ratio of the carbonic acid diester and the aromaticdihydroxy compound for obtaining the aromatic polycarbonate oligomeraccording to the present invention, the carbonic acid diester is usually0.5 to 1.5 times by mol, preferably 0.6 to 1.2 times by mol, relative to1 mol of the aromatic dihydroxy compound.

In melt transesterification reaction, a transesterification catalyst isused, if necessary, in order to increase the reaction rate.

The transesterification catalyst is not particularly limited, and it ispossible to use a known transesterification catalyst such as alkalimetal compounds such as inorganic alkali metal compounds such ashydroxides, carbonates, and hydrogencarbonate compounds of lithium,sodium, and cesium, and organic alkali metal compounds such asalcoholates and organic carboxylic acid salts; alkaline earth metalcompounds such as inorganic alkaline earth metal compounds such ashydroxides and carbonates of beryllium, magnesium, and the like andorganic alkaline earth metal compounds such as alcoholates and organiccarboxylic acid salts; basic boron compounds such as sodium salts,calcium salts, and magnesium salts of tetramethylboron, tetraethylboron,butyltriphenylboron, and the like; basic phosphorus compounds such astrivalent phosphorus compounds such as triethylphosphine andtri-n-propylphosphine and quaternary phosphonium salts derived fromthese compounds; basic ammonium compounds such as tetramethyl ammoniumhydroxide, tetraethyl ammonium hydroxide, and tetrabutyl ammoniumhydroxide; or amine compounds such as 4-aminopyridine,2-dimethylaminoimidazole, and aminoquinoline. Among them, alkali metalcompounds are preferable, and cesium compounds such as cesium carbonateand cesium hydroxide are particularly preferable.

As the amount of the catalyst to be used, the catalyst is used in arange in which a catalyst residue does not cause quality problems of theproduced oligomer, and although it cannot be said unconditionallybecause the suitable amount to be added varies depending on the kind ofthe catalyst, the amount is usually 0.05 to 100 μmol, preferably 0.08 to50 μmol, more preferably 0.1 to 20 μmol, still more preferably 0.1 to 5μmol, relative to 1 mol of the aromatic dihydroxy compound, for example.

The catalyst may be added as it is or may be added by being dissolved ina solvent, and the solvent is preferably, for example, one which doesnot affect the reaction such as water, phenol, and the like.

As the reaction condition of the melt transesterification reaction, thetemperature is usually in the range of 120 to 360° C., preferably in therange of 150 to 280° C., more preferably in the range of 180 to 260° C.If the reaction temperature is too low, the transesterification reactiondoes not proceed, and if the reaction temperature is high, sidereactions such as decomposition reaction proceed; therefore, it is notpreferable. The reaction is preferably carried out under reducedpressure. The reaction pressure is preferably a pressure at whichcarbonic acid diester as a raw material does not distill out of thesystem and the by-produced phenol distills, at the reaction temperature.Under such reaction conditions, the reaction is usually completed inabout 0.5 to 10 hours.

Then, a separation process is carried out using a final reaction productobtained in the above reaction process.

The final reaction product containing the aromatic polycarbonateoligomer obtained by the above reaction process is usually a transparentviscous substance in a molten state around the reaction temperature andis a solid around ordinary temperature. By treating the final reactionproduct having such properties with a specific solvent and drying thereaction product, it is possible to obtain the solid of the presentinvention in which the low molecular weight components according to thepresent invention are remarkably reduced and the loose bulk density ishigh and which is an easy-to-handle powder or the like.

Although there are no particular restrictions on the method in theseparation process of separating from the above-described final reactionproduct, for example, it is preferable that a solution is prepared bydissolving the entire final reaction product containing a low molecularweight component in a solvent (good solvent) which can dissolve thefinal reaction product well, then this solution is mixed with a solvent(poor solvent), which has a very low solubility for an aromaticpolycarbonate oligomer but selectively dissolves the low molecularweight component, to dissolve and separate the low molecular weightcomponent and to precipitate oligomer, or the final reaction product isdirectly mixed in a slurry state in a poor solvent to dissolve andseparate the low molecular weight component in the poor solvent and toobtain the oligomer as a precipitate, and thus to separate by filtrationand dry, whereby the aromatic polycarbonate oligomer solid of thepresent invention having a high loose bulk density is obtained. Ifnecessary, the separation process may be repeated a plurality of timesusing the obtained aromatic polycarbonate oligomer.

The good solvent is a solvent which dissolves both the polycarbonateoligomer and the low molecular weight component well. Specific examplesthereof include aromatic hydrocarbon solvents such as toluene and xyleneand aliphatic ketone solvents having 1 to 8 carbon atoms such asacetone, methyl ethyl ketone, and methyl isobutyl ketone. Ahalogen-containing solvent such as dichloromethane and tetrahydrofuranare not suitable as good solvents, because chlorine component residue ismixed in the obtained solid and the loose bulk density is low.

On the other hand, the poor solvent is a solvent which has a very lowsolubility for the polycarbonate oligomer but dissolves the lowmolecular weight component and in addition can obtain a solid in whichthe loose bulk density of the polycarbonate oligomer solid afterseparation and drying is high. Specific examples thereof includealiphatic alcohol solvents having 1 to 6 carbon atoms such as methanol,ethanol, and propanol and mixtures of the aliphatic alcohol solvents andwater.

When the solvent used as a good solvent is a water-soluble ketonesolvent such as acetone, water alone may be used as a poor solvent.

In the above separation process, a method in which the entire finalreaction product is dissolved in a good solvent to prepare a solution,then this solution is mixed with a poor solvent to dissolve and separatethe low molecular weight component, and the oligomer can be precipitatedwill be described in more detail. The entire final reaction product isheated, if necessary, and dissolved in a good solvent using, forexample, a vessel equipped with a temperature raising device, a stirrer,and a condenser, and the solution is added dropwise to a poor solvent,or vice versa, the poor solvent is added dropwise to the solution toprecipitate the aromatic polycarbonate oligomer and thus to separate theprecipitate by filtration.

Here, although the amount ratio of the good solvent and the poor solventto the final reaction product is not particularly limited, if the amountof the good solvent is too large, the yield is reduced, whereas if theamount of the poor solvent is too large, solvent recovery costincreases, which is not preferable.

Accordingly, with respect to the final reaction product, preferably, thegood solvent is used in the range of 0.5 to 20 times by weight, and thepoor solvent is used in the range of 0.5 to 50 times by weight. Morepreferably, the good solvent is used in the range of 0.6 to 15 times byweight, and the poor solvent is used in the range of 0.6 to 30 times byweight. Particularly preferably, the good solvent is used in the rangeof 0.7 to 12 times by weight, and the poor solvent is used in the rangeof 1.0 to 25 times by weight.

The weight of the poor solvent with respect to the weight of the goodsolvent is preferably in the range of 1.0 to 20 times by weight, morepreferably 2.0 to 10 times by weight, particularly preferably 3.0 to 8.0times by weight.

A method in which the final reaction product is directly mixed in aslurry state in a poor solvent to dissolve and separate the lowmolecular weight component in the poor solvent and to precipitate theoligomer will be described in more detail. When the entire finalreaction product is a viscous substance in a molten state, the finalreaction product is used as it is, or when the entire final reactionproduct is a solid, the final reaction product is crushed appropriately,if necessary. The final reaction product is heated if necessary, using,for example, a vessel equipped with a temperature raising device, astirrer, and a condenser, added into the poor solvent under stirring,and made into a slurry state to dissolve and separate the low molecularweight component in the poor solvent, and the aromatic polycarbonateoligomer is precipitated to be separated by filtration. Here, althoughthe amount ratio of the poor solvent to the final reaction product isnot particularly limited, if the amount of the poor solvent is toolarge, the solvent recovery cost increases, which is not preferable.

Accordingly, the poor solvent is used preferably in the range of 1 to 50times by weight, more preferably in the range of 1 to 30 times byweight, particularly preferably in the range of 2 to 20 times by weightwith respect to the final reaction product.

The temperature and time for carrying out the separation by dissolutionand precipitation operation in the above separation process are notparticularly limited and may vary depending on the solvent used and thetype of final reaction product, but are usually set within the range of0 to 100° C. and 1 to 40 hours respectively.

The solution in which the low molecular weight component is dissolved isseparated from a precipitate by using a filtration filter or the like,only the solution is removed, and the residue is dried using a dryersuch as a vacuum dryer or a hot air dryer, so that the low molecularweight components in the present invention are reduced, and an aromaticpolycarbonate oligomer having a high loose bulk density is obtained.

Next, a method of obtaining the aromatic polycarbonate oligomeraccording to the present invention by the interfacial polymerizationmethod will be described. In the interfacial polymerization method, aconventionally known method of reacting an aromatic dihydroxy compoundwith a carbonate precursor such as phosgene under an inert solvent canbe used.

In the polymerization reaction, for example, pH is usually maintained at9 or more in the presence of an organic solvent inert to the reactionand an alkaline aqueous solution, and1,1-bis(4-hydroxyphenyl)-1-phenylethane represented by the above formula(2) and, if necessary, a molecular weight regulator (terminator) areused and reacted with phosgene. Then, a polymerization catalyst such asa tertiary amine or a quaternary ammonium salt is added, and interfacialpolymerization is performed to obtain a polycarbonate oligomer.

The addition of the molecular weight regulator is not particularlylimited as long as it is performed from the time of phosgenation to thestart of the polymerization reaction. The reaction temperature isusually 0 to 40° C., and under such reaction conditions, the reaction iscompleted in about 10 minutes to 6 hours.

Specific examples of the organic solvent inert to the reaction includechlorinated hydrocarbons such as dichloromethane, 1,2-dichloroethane,chloroform, monochlorobenzene, and dichlorobenzene and aromatichydrocarbons such as benzene and toluene. Examples of an alkali compoundused for trapping hydrogen chloride generated by the reaction includealkali metal hydroxides such as sodium hydroxide and potassiumhydroxide.

Examples of the molecular weight regulator include a compound having amonovalent phenolic hydroxyl group, and specific examples thereofinclude phenol, m-methylphenol, p-methylphenol, m-propylphenol,p-propylphenol, p-tert-butylphenol, and p-long-chain alkyl-substitutedphenol. The amount of the molecular weight regulator to be used ispreferably 50 to 0.5 mol, particularly preferably 30 to 1 mol, relativeto 100 mol of the aromatic dihydroxy compound.

Examples of the polymerization catalyst include tertiary amines such astrimethylamine, triethylamine, tributylamine, tripropylamine,trihexylamine, and pyridine; and quaternary ammonium salts such astrimethylbenzylammonium chloride, tetramethylammonium chloride, andtriethylbenzylammonium chloride.

In the interfacial polymerization method, the final reaction productcontaining the polycarbonate oligomer is usually obtained as solution ofa chlorine type organic solvent such as dichloromethane or an aromatichydrocarbon type organic solvent such as benzene. Accordingly, in orderto obtain a polycarbonate oligomer solid, it is necessary to separatethe polycarbonate oligomer from the solution and dry the polycarbonateoligomer, and as the separation method, “gel concentration method”(solvent distillation gelation, flash concentrated gelation, etc.), “hotwater dropping method”, “precipitation method”, and the like are known.However, the polycarbonate oligomer obtained by separation and drying inthis way in the prior art has a lot of impurities, such as chlorinecomponent residue, low molecular weight component residue, and residuedue to high temperature thermal history in a dryer, and is a solid whichis in a powder state or the like and which has a low loose bulk density.Therefore, in the separation process in the present invention, thepolycarbonate oligomer solid obtained from the final reaction product isdissolved in a specific solubilizing solvent (good solvent), and thenthis is subjected to precipitation treatment in a specific precipitatingsolvent (poor solvent), or the polycarbonate oligomer solid obtainedfrom the final reaction product is subjected to slurry treatment in thepoor solvent and dried. By performing such a separation process, it ispossible to obtain the solid of the present invention in which the lowmolecular weight components are remarkably reduced, thechlorine-containing compound is not present or is remarkably reduced,and the loose bulk density is high and which is an easy-to-handle powderor the like.

Although a method in the separation process of obtaining the solid ofthe present invention from the polycarbonate oligomer solid obtainedfrom the final reaction product is not particularly limited, thepreferred method is the same as the method in the separation process ofobtaining the solid of the present invention from the final reactionproduct in the melt transesterification method, and the preferred goodsolvent and poor solvent and the separation conditions and the like arethe same thereas.

The use of the compound of the present invention obtained as describedabove will be described.

The polycarbonate oligomer of the present invention can be used as a rawmaterial in producing a high molecular weight polycarbonate by variouspolymerization methods, and in particular, an aromatic polycarbonateobtained by the melt polymerization method or the solid phasepolymerization method, using the compound of the present invention as araw material has excellent transparency, heat resistance, mechanicalproperties, impact resistance, fluidity, and the like, and can beexpected to be used in optical applications such as optical discs andlenses and various fields such as automobile field, electric/electronicfield, and various containers as engineering plastics.

The compound of the present invention can be widely used as an additivesuch as a surface modifier, a flame retardant, an ultraviolet absorber,a fluidity modifier, a plasticizer, or a polymer modifier such as aresin alloy compatibilizer.

In addition, the compound of the present invention can also be used asvarious resin raw materials other than polycarbonate. In that case, thecompound of the present invention can be used as it is or afterprocessing.

EXAMPLES

Hereinafter, the present invention will be specifically described withreference to examples, but the present invention is not limited to theseexamples.

In the following examples, the weight average molecular weight wasmeasured by gel permeation chromatography, the low molecular weightcomponent was measured by area % of high performance liquidchromatography, and the loose bulk density was measured by the followingmethod. The analysis method is as follows.

<Analysis Method> 1. Gel Permeation Chromatography Measurement

Apparatus: HLC-8320 GPC manufactured by Tosoh Corporation

Flow rate: 0.35 ml/min, Mobile phase: tetrahydrofuran, Amount ofinjection: 10 μl

Column: TSKgel guard column Super MP(HZ)-N, TSKgel SuperMultipore HZ-N×3columns

Detector: RI, Analysis method: Relative molecular weight in polystyreneequivalent. As polystyrene standards, A-500, A-2500, A-5000, F-1, F-2and F-4 manufactured by Tosoh Corporation were used.

2. High Performance Liquid Chromatography Measurement

Apparatus: LC-10Avp series manufactured by Shimadzu Corporation

Pump: LC-10 ATvp

Column oven: CTO-10 Avp

Detector: SPD-10 Avp

Column: Shim-pack CLC-ODS inner diameter 6 mm, length 150 mm

Oven temperature: 50° C.

Flow rate: 1.0 ml/min

Mobile phase: (A) tetrahydrofuran, (B) 0.1 vol % aqueous phosphoric acid

Gradient condition: (A) volume % (time from start of analysis)

40% (0 min)→65% (10 min)→70% (20 min)→70% (40 min)→100% (50 min)→100%(60 min)

Sample injection amount: 20 μl

Detection wavelength: 254 nm

3. Loose Bulk Density Measurement

Polycarbonate oligomer was placed in a measuring cylinder, and thevolume (cm³) and weight (g) of the contents were measured.

*Loose bulk density (g/cm³)=weight (g)/volume (cm³)

Example 1

135.6 g (0.47 mol) of 1,1-bis(4-hydroxyphenyl)-1-phenylethane and 70.0 g(0.33 mol) of diphenyl carbonate were charged into a four-necked flaskequipped with a thermometer, a stirrer, a cooler, and after the insideof a reaction vessel was replaced with nitrogen, 0.5 g of a 0.06% cesiumcarbonate aqueous solution was added at 98° C. After the temperature wasraised to 200° C., the reaction was carried out at a degree of pressurereduction adjusted to 1.3 kPa for 2 hours. Further, after thetemperature was raised to 220° C., the reaction was carried out at adegree of pressure reduction adjusted to 0.3 kPa for 3 hours whiledistilling out the phenol formed. The low molecular weight component of129.4 g of the final reaction solution obtained was 26.8% (highperformance liquid chromatography area %).

Subsequently, a solution prepared by dissolving 54.0 g of the obtainedfinal reaction solution in 108.2 g of methyl isobutyl ketone was addeddropwise to 648.2 g of methanol charged in a four necked flask over 2hours while maintaining the temperature at 15° C., and precipitationoperation was carried out. After stirring overnight, the precipitate wasseparated by filtration and dried to obtain 36.8 g of a powdered crudeproduct (a).

A solution prepared by dissolving 30.0 g of the obtained crude product(a) in 90.0 g of methyl isobutyl ketone was added dropwise to 330.2 g ofmethanol charged in a four necked flask over 2 hours while maintainingthe temperature at 15° C., and reprecipitation operation was carriedout. After stirring overnight, the precipitate was separated byfiltration and dried to obtain 26.9 g of a powdered crude product (b).

18.0 g of the obtained crude product (b) and 216.0 g of methanol werecharged in a four-necked flask, and after stirring overnight at 20° C.,the precipitate was separated by filtration and dried to obtain 16.6 gof polycarbonate oligomer.

The weight average molecular weight of the obtained polycarbonateoligomer was 3096 (gel permeation chromatography), the low molecularweight component was 0.8% (high performance liquid chromatography area%), and the loose bulk density was 0.36 g/cm³.

Comparative Example 1

A solution prepared by dissolving 10.0 g of the final reaction solution(low molecular weight component was 26.8%) obtained in the same manneras in Example 1 in 38.0 g of dichloromethane was added dropwise to 120.0g of hot water at 45° C. charged in a four-necked flask over 1 hour, anda solvent was removed to solidify a polymer. However, polycarbonateoligomer was not dispersed and became a resinous mass. After allowed tostand overnight, a solid of the resinous mass was isolated, and thecrushed solid was analyzed.

The weight average molecular weight of the obtained polycarbonateoligomer was 2185 (gel permeation chromatography), and the low molecularweight component was 26.6% (high performance liquid chromatography area%). Since a resinous mass was obtained, the loose bulk density could notbe measured.

Comparative Example 2

A solution prepared by dissolving 20.0 g of the final reaction solution(low molecular weight component was 26.8%) obtained in the same manneras in Example 1 in 176.0 g of dichloromethane was added dropwise to1958.0 g of methanol charged in a four-necked flask over 2 hours at 15°C., and precipitation operation was carried out. After stirringovernight, the precipitate was separated by filtration and dried toobtain 11.0 g of a crude product.

A solution prepared by dissolving 9.1 g of the obtained crude product in145.2 g of dichloromethane was added dropwise to 1615.4 g of methanolcharged in a four-necked flask over 2 hours at 15° C., andreprecipitation operation was carried out. After stirring overnight, theprecipitate was separated by filtration and dried to obtain 7.9 g ofpowdered polycarbonate oligomer.

The weight average molecular weight of the obtained polycarbonateoligomer was 3319 (gel permeation chromatography), the low molecularweight component was 0.1% (high performance liquid chromatography area%), and the loose bulk density was 0.28 g/cm³.

1. An aromatic polycarbonate oligomer solid comprising a repeating unitrepresented by the following formula (1) and having a weight averagemolecular weight of 500 to 10000, a low molecular weight component of5.0 area % or less as measured by high performance liquidchromatography, and a loose bulk density of 0.30 g/cm³ or more,


2. An aromatic polycarbonate oligomer solid obtained from an aromaticdihydroxy compound represented by the following formula (2) and acarbonic acid diester and having a weight average molecular weight of500 to 10000, a low molecular weight component of 5.0 area % or less asmeasured by high performance liquid chromatography, and a loose bulkdensity of 0.30 g/cm³ or more,